Slurry for use in polishing semiconductor device conductive structures that include copper and tungsten and polishing methods

ABSTRACT

method for substantially simultaneously polishing a copper conductive structure of a semiconductor device structure and an adjacent barrier layer. The method includes use of a polishing pad with a slurry solution in which copper and a material, such as tungsten, of the barrier layer are removed at substantially the same rate. The slurry is formulated so as to oxidize copper and a material of the barrier layer at substantially the same rates. Thus, copper and the barrier layer material have substantially the same oxidation energies in the slurry. Systems for substantially polishing copper conductive structures and adjacent barrier structures on semiconductor device structures are also disclosed.

FIELD OF THE INVENTION

The present invention relates generally to slurries that are useful in chemical-mechanical polishing or chemical mechanical planarization processes and, more specifically, to slurries that are used to polish or planarize electrically conductive structures of semiconductor devices that include copper and an adjacent tungsten-containing barrier. The present invention also relates to methods for substantially concurrently polishing or planarizing structures formed from copper and tungsten.

BACKGROUND OF THE INVENTION

CMP

Chemical-mechanical polishing and chemical-mechanical planarization, both of which are referred to in the art as “CMP”, are abrasive techniques that typically include the use of a combination of chemical and mechanical agents to planarize, or otherwise remove material from or planarize a surface of a semiconductor material substrate during the fabrication of devices thereon. A chemical component, typically a slurry that includes one or more oxidizers, abrasives, complexing agents, and inhibitors, oxidizes the surface of one or more material layers that are being polished or planarized (i.e., at least partially removed). A polishing pad formed from a material such as polyurethane or acrylic is used with the slurry and, in combination with abrasives present in the slurry, effects mechanical removal of the layer or layers from the surface of the semiconductor device structure. It should be noted that abrasive-only polishing and planarization, e.g., without the use of active chemical agents to effect material removal, are becoming more prevalent due to environmental concerns. Thus, the term “CMP” as used herein encompasses such abrasive-only (i.e., strictly mechanical) methods and apparatus.

Copper Conductive Structures

The use of copper as a conductive material in semiconductor devices is also ever increasing. When copper is used in semiconductor devices, however, a barrier layer is typically required between the copper and adjacent structures or layers. The barrier layer prevents diffusion of the copper into the adjacent layers or structures, as well as the formation of copper silicides, both of which may cause electrical shorts in semiconductor devices that include copper. Tantalum is an example of a material that is useful as a copper barrier. When tantalum is used, the semiconductor device, including any features thereof into which copper is to be disposed (e.g., trenches), is lined with a layer of tantalum. The tantalum layer is then typically covered with a thin copper layer, often formed by physical vapor deposition (“PVD”) processes. The thin copper layer then acts as a so-called “seed layer” for the formation of a copper structure, such as a conductive line, such as by electroplating processes.

Once the tantalum and copper layers have been formed, it is necessary to isolate separate tantalum-copper conductive structures from one another. CMP processes are typically used to remove the tantalum and copper between the structures from over the active surface of the semiconductor device being fabricated. Slurries that are used in copper CMP processes typically have a pH of about 7.0. Many of these slurries include hydrogen peroxide (H₂O₂) as an oxidizing agent. Since hydrogen peroxide readily generates hydroxy free radicals (OH), hydrogen peroxide is a very strong oxidizing agent. Tantalum, however, is substantially chemically inert. Thus, the oxidizers of CMP slurries that remove copper do not effectively oxidize tantalum and, thus, do not adequately effect the removal of tantalum. Likewise, slurries that are useful for removing tantalum by CMP processes are likewise not effective for removing copper. As a result, when conventional CMP processes are used to isolate the tantalum-copper conductive structures of a semiconductor device, two separate slurries must be used.

It has been proposed that tungsten be used in place of tantalum in semiconductor devices as a barrier material for copper conductive structures. Nonetheless, when known copper CMP slurries are used to substantially simultaneously CMP tungsten and copper, the tungsten barrier layer may dissolve, or be removed, at a faster rate than the copper. This is at least partially because, as the following chemical equations illustrate, tungsten (W) is more readily oxidized than copper (Cu):

W+2H₂O→4H++4e ⁻+WO₂ E_(o)=0.12;

Cu→Cu²⁺+2e ⁻E_(o)=−0.34.

Thus, in conventional slurries, although both copper and tungsten are simultaneously exposed to the same oxidants, the tungsten will typically be oxidized first. As a result, gaps may form in locations where the barrier material should be located between copper conductive structures and adjacent portions of the semiconductor device structure upon which the conductive structures are being fabricated.

This phenomenon is illustrated in the electron micrograph of FIG. 1, which illustrates a semiconductor device structure 10 that includes the portions of a copper layer 20 and an underlying tungsten barrier layer 18 disposed within a recess 14 formed in an active surface 16 of a substrate 12 of semiconductor device structure 10 following CMP thereof using an alumina fixed-abrasive polishing pad and a copper CMP slurry having a pH of about 7. Once an interface 19 between barrier layer 18 and copper layer 20 was exposed during the CMP process, tungsten of barrier layer 18 was oxidized and dissolved at a faster rate than the adjacent copper of copper layer 20, leaving a gap 21 between copper layer 20 and adjacent regions of substrate 12, as well as undesirably permitting copper of copper layer 20 to contact and, possibly, diffuse into, unprotected adjacent regions of substrate 12.

Therefore, it would is desirable to provide a slurry that is useful in CMP processes and that effectively polishes or planarizes both copper and tungsten without causing oxidation or dissolution of the tungsten.

SUMMARY OF THE INVENTION

The present invention includes a method for substantially simultaneously chemical-mechanical polishing a copper conductive structure and an adjacent barrier layer with a polishing pad, as well as slurries that are useful for substantially simultaneously polishing a copper conductive structure and a barrier layer adjacent thereto.

The method of the present invention includes employing a polish pad along with a liquid polishing formulation, which is generally referred to herein as a slurry. The slurry is formulated to oxidize copper and a material of the barrier layer, such as tungsten, at substantially the same rates and without preference between the two materials. Thus, in a slurry incorporating teachings of the present invention, the oxidation energies of copper and the barrier material are substantially the same. Preferably, in the slurry, the oxidation energy of a barrier material, such as a tungsten-containing material (e.g., tungsten (W) and tungsten nitride WN_(x)) is about 0.25 volt greater to about 0.2 volt less than an oxidation energy of copper. As copper and the barrier material are oxidized by the slurry at about the same rates, use of a slurry so formulated to substantially simultaneously polish a copper conductive structure and an adjacent barrier layer, prevents dissolution of the barrier layer.

Slurries that are useful in the method of the present invention include at least one oxidizer, at least on inhibitor, and one or more abrasives, and optionally but preferably one or more complexing agents. The relative amounts of the oxidizer, inhibitor, abrasive, and optional complexing agent, are balanced so as to facilitate substantially concurrent polishing of a copper structure and another structure adjacent thereto, such as a barrier layer formed from a tungsten-containing material. Thus, the slurry is formulated such that the relative amounts of the oxidizer, inhibitor, abrasive, and optional complexing agent, to oxidize copper and a barrier material, such as a tungsten-containing material, at substantially the same rates, or such that the oxidation energies of copper and the barrier material are substantially the same in the slurry, and to polish or planarize the surface of the wafer or other structure. The pH of the slurry is also be optimized so as to provide for oxidation of copper and a barrier material, such as a tungsten-containing material, at substantially the same rates.

With such exemplary solutions in accordance with the invention received intermediate the wafer and polishing pad, the copper comprising layer is chemical-mechanical polished with slurry and the polishing pad. The slurries can be utilized with a conventional planarizing machine known and used in the art for chemical-mechanical polishing a semiconductor wafer.

The present invention also includes a system for substantially simultaneously polishing a copper conductive structure and an adjacent barrier layer of a semiconductor device. Such a system includes a polishing pad and a slurry according to the invention, within which copper and the material of the barrier layer are oxidized at substantially the same rates, or have substantially the same oxidation energies.

Other features and advantages of the present invention will become apparent to those of ordinary skill in the art through consideration of the ensuing description, the accompanying drawings, and the appended claims.

BRIEF DESCRIPTION OF THE DRAWINGS

Preferred embodiments of the invention are described below with reference to the following accompanying drawings.

FIG. 1 is an electron micrograph illustrating the dissolution of regions of a tungsten barrier layer that underlie a copper structure of a semiconductor device structure when a conventional slurry is used to simultaneously remove the copper and tungsten;

FIGS. 2-5 schematically illustrate an exemplary embodiment of a polishing method in which copper and a barrier material therefor are substantially simultaneously removed from a semiconductor device structure at substantially the same rates; and

FIG. 6 is a schematic representation of an exemplary embodiment of a system that employs a polishing pad and a slurry to effect the method of the present invention.

FIG. 7 is a schematic representation of an exemplary embodiment of a system that employs a web-format planarizing machine to effect the method of the present invention.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

A method incorporating teachings of the present invention is illustrated in FIGS. 2-5. With reference to FIG. 2, a semiconductor device structure 10 including a substrate 12, which includes a recess 14 formed in an active surface 16 thereof. A barrier layer 18 of a material, such as a tungsten-containing material, that prevents copper from diffusing into adjacent insulative regions of semiconductor device structure 10 located on active surface 16 and on the surfaces 15 of recess 14. Preferably, the tungsten-containing material comprises greater than about 50% tungsten. Exemplary tungsten-containing materials include tungsten (W) and tungsten nitride having the formula WN_(x). A copper layer 20 is formed over and contacts barrier layer 18. Copper layer 20 also substantially fills recess 14. Although substrate 12 may include various other structures beneath recess 14, barrier layer 18, and copper layer 20, for purposes of simplicity, no additional structures are illustrated in the semiconductor device structure 10 shown in FIGS. 2-5.

In forming a conductive structure from copper layer 20, portions of copper layer 20 and of barrier layer 18 that are not located within recess 14 must be removed from semiconductor device structure 10. As discussed previously herein, CMP processes are typically used to remove unwanted portions of copper layers. With reference to FIG. 3, a slurry 30 is applied over copper layer 20. A polishing pad 40, which may be embodied as a conventional polishing pad, a web-type polishing pad, a belt-type polishing pad, or in any other polishing pad format known in the art, is then brought into frictional contact (e.g., by rotation of semiconductor device structure 10 or movement of the polishing pad 40) with copper layer 20 to, along with slurry 30, remove copper layer 20. An inhibitor component 32 of slurry 30 fills recessed areas 22 of copper layer 20, thereby preventing removal of material from recessed areas 22 until material of higher areas 24 of copper layer 20 has been removed.

Eventually, regions of barrier layer 18 overlying active surface 16 are exposed through copper layer 20, as shown in FIG. 4. At this point, slurry 30 and polishing pad 40 remove the material or materials of barrier layer 18 and the copper of copper layer 20 at substantially the same rates.

Barrier layer 18 is removed from active surface 16 by continued polishing with slurry 30 and polishing pad 40. Once barrier layer 18 is substantially removed from active surface 16 and the surface 26 of the portion of copper layer 20 that remains within recess 14 is located substantially in the plane of active surface 16, as depicted in FIG. 5, the polishing process is terminated. As illustrated in FIG. 5, the remaining portion of barrier layer 18 substantially lines recess 14 and separates the remaining portion of copper layer 20 from adjacent portions of substrate 12.

In order to effect removal of copper and the material or materials (e.g., tungsten-containing material) of an adjacent barrier layer 18 or other structure by CMP at substantially the same rates, slurry 30 is formulated so as to oxidize copper and the material or materials of the adjacent barrier layer 18 at substantially the same rates. Stated another way, copper and the material or materials (e.g., tungsten-containing material) of the adjacent barrier layer 18 have substantially the same oxidation energies in slurry 30. As a result, as an interface 19 between layers 18 and 20 is exposed to slurry 30, the material or materials of barrier layer 18 will not dissolve, or be removed from semiconductor device structure 10, at a significantly greater rate than copper or copper layer 20 is dissolved, or removed from semiconductor device structure 10. To achieve the desired removal, the oxidation energy of the tungsten-comprising material in slurry 30 is preferably about 0.25 volt more to about 0.2 volt less than the oxidation energy of copper in slurry 30.

Slurry 30 includes an oxidizer component, which oxidizes both the copper of copper lay 20 and the material or materials (e.g., tungsten-containing material) of barrier layer 18 so as to chemically soften these materials and to thereby facilitate their mechanical removal from semiconductor device structure 10 by polishing pad 40. Slurry 30 includes an inhibitor component 32, which prevents recessed, or lower, areas 22 of copper layer 20 from being removed until higher areas 24 of copper layer 20 have been removed down to substantially the same plane. Slurry 30 further includes an abrasive agent, which effects the mechanical part of the CMP process to abrade and polish or planarize the surface of the semiconductor device 10, in combination with polishing pad 40. As a result, the continued oxidation of material layers 18, 20 by slurry 30 may occur at optimal rates and, thus, the rates at which the materials of layers 18 and 20 are removed from semiconductor device structure 10 may also be optimized.

According to the invention, to achieve an optimal and balanced rate of removal of the copper and tungsten-containing barrier layers at substantially the same rates, and without preferential etching of one material over the other, the slurry is formulated to achieve a ΔE range of about 0.05 eV to about 0.20 eV, by optimizing the oxidizer component and the pH of the slurry.

The amount of oxidizer included in the slurry is controlled to maintain an about equal rate of selectivity between the copper of copper layer 20 and the material or materials (e.g., tungsten-containing material) of barrier layer 18. Examples of oxidizers that are useful as the oxidizer component of slurry 30 include, without limitation, hydrogen peroxide, ammonium persulfate, potassium iodate, potassium permnanganate, ferric nitrate, and cerium (IV) compounds such as ceric nitrate and ceric ammonium nitrate, bromates, chlorates, chromates, and iodic acid, and mixtures thereof. The oxidizer component preferably comprises about 0.05% to about 10% by weight of slurry 30, preferably about 0.1% to about 5.0% by weight, more preferably about 3% to about 5% of the weight of slurry 30. The oxidizing agent is preferably not as strong as, for example, hydrogen peroxide or an organic peroxide such as monopersulfates, which have a relatively high static etch rate of the tungsten-containing material. Thus, a “dual” oxidizer can be used comprising the foregoing oxidizing agents combined with a minimal amount of hydrogen peroxide or ammonium persulfate, of about 0.001% to about 1% by weight of the slurry.

Examples of useful copper corrosion inhibitors 32 include azoles such as imidazole, benzotriazole, benziimidazole, benzothizole, mercaptabenzothiazole and tolytriazole, and other azole derivatives with hydroxy, amino, imino, carboxy, mercapto, nitro and alkyl substituted groups; urea and thiourea; amines such as methylamine and diethylamine; ring compounds such as pyridine, quinoline, and dicyclohexamine nitrite; other compounds such as potassium silicate, ammonium borate, ammonium phosphate and potassium dichromate; and mixtures thereof. Inhibitor component 32 of slurry 30 preferably includes an azole compound, such as benzenetriazole (BTA). While inhibitor component 32 may make up about 0.05% to about 2% by weight of slurry 30, it is preferred the inhibitor component 32 comprise about 0.05% to about 0.2% by weight of slurry 30. For example, slurry 30 may include about 0.1% BTA, by weight.

Examples of useful abrasive agents include, but are not limited to, alumina (Al₂O₃), titanium dioxide (TiO₂), silicon dioxide (SiO₂), and cerium dioxide (CeO₂). The abrasive preferably comprises about 0.5% to about 10% by weight of slurry 30.

Slurry 30 can have a pH in the range of about 3 to about 7, but the pH of slurry 30 is optimally in the range of about 3 to about 5. One or more pH control agents or buffers may be used, as known in the art, to adjust the pH of slurry 30 to a desired level. Preferably, the pH control agent will adjust the pH of slurry 30 to a desirable range or point without significantly etching the insulator (e.g., borophosphosilicate glass (BPSG), phosphosilicate glass (PSG), or borosilicate glass (BSG)) that underlies the layer or layers being polished. Examples of useful pH control agents include potassium hydrogen phthalate, ammonium phosphate, ammonium acetate, ammonium dihydrogen phosphate, dibasic ammonium citrate, ammonium hydrogen phosphate, tribasic ammonium citrate, ammonium oxalate, ammonium carbamate, acetic acid, phosphoric acid, and sulfuric acid, among others, and mixtures thereof.

In a preferred embodiment, slurry 30 also includes one or more complexing agents, which complex with ions of the layers 18, 20 being removed (e.g., copper ions from copper layer 20) so as to facilitate the dissolution of these reactant ions, allowing these reactant ions to be moved away from the locations at which layers 18 and 20 are being oxidized. Examples of suitable complexing agents of slurry 30 may include, but are not limited to, glycine, ammonium citrate, ammonium phosphate, ammonium acetate, ammonium thiocyanate, and 2,4-pentadione, and combinations thereof. Slurry 30 preferably includes about 1% to about 10% of the one or more complexing agents, by weight of slurry 30, more preferably about 3% to about 5% by weight of slurry 30. For example, slurry 30 may include about 1% of the complexing agent glycine, including a concentration of 0.1 M (molar) polyethylene glycol (PEG), by weight of slurry 30. As another example, slurry 30 may include about 3% ammonium acetate, by weight.

The slurry solution can also comprise one or more surfactants, for example present at a concentration of from about 1% to about 10% by volume. Example surfactants include dodecyl sulfate sodium salt, sodium lauryl sulfate, dodecyl sulfate ammonium salt, polyethylene glycol, polyoxyethylene ether, glycerol, polypropylene glycol, polyoxyethylene lauryl ether, polyoxyethylene cetyl ether, polyoxyethylene stearyl ether, polyoxyethylene oleyl ether, and mixtures thereof. The slurry can further comprise one or more thickeners to achieve a desired viscosity, with an example preferred range being from about 10 centipoise to about 20 centipoise at room temperature. Examples of suitable thickeners include Polyox™ available from Union Carbide of Danbury, Conn., and Carbopol™ available from B.F. Goodrich of Cleveland, Ohio.

The specific amounts of the components of slurry 30 may be determined by identifying slurry 30 formulations in which copper gives up electrons at substantially the same rate as a barrier material, such a tungsten-containing material, of a barrier layer 18 to be polished substantially simultaneously with copper layer 20. Stated another way, slurry 30 may be formulated so that copper and a barrier material therefor, such as a tungsten-containing material, have the substantially same oxidation energies therein, or are oxidized at substantially the same rates therein. Preferably, the oxidation energy of the tungsten-containing material or another barrier material in slurry 30 is within the range of about 0.25 volt more than to about 0.2 volt less than the oxidation energy of copper in slurry 30, the range including the end point values thereof. These formulations of slurry 30 will facilitate the removal of copper and a barrier material, such as a tungsten-containing material, from a semiconductor device structure 10 at substantially the same rates.

Slurry 30 formulations having these characteristics may be determined as known in the art, such as by measuring the open circuit potentials of copper and a barrier material, such as tungsten, in slurry 30.

Referring now to FIG. 6, a polishing system 50 for effecting the substantially simultaneous polishing of copper and an adjacent barrier material in accordance with the method of the present invention is illustrated. Polishing system 50 includes a polishing apparatus 42, which supports or carries a polishing pad 40, and a substrate support 44 configured to hold a semiconductor device structure 10, to bring the same into frictional contact with polishing pad 40, and, preferably, to rotate semiconductor device structure 10 relative to polishing pad 40. Polishing system 50 also includes a slurry applicator 46 and a rinsing element 48.

Any known CMP apparatus, including conventional, rotary CMP apparatus, web format CMP apparatus, and belt format CMP apparatus, may comprise polishing apparatus 42, substrate support 44, slurry applicator 46, and rinsing element 48 of polishing system 50.

Conventional CMP pads are round, planar, and have larger dimensions than the semiconductor substrates (e.g., wafers or other substrates including silicon, gallium arsenide, indium phosphide, etc.) upon which the structures or layers to be planarized or otherwise polished have been formed. In polishing one or more layers or structures formed on a substrate, the substrate and the conventional CMP pad are rotated relative to one another, with the location of the substrate being moved continuously relative to the polishing surface of the pad so that different areas of the pad are used to polish one or more of the layers or structures formed on the substrate.

In use of polishing system 50, one or more semiconductor device structures 10 having one or more layers thereon that are to be chemical-mechanical polished are secured to substrate support 44. If necessary, polishing pad 40 is also secured to polishing apparatus 42. Slurry 30 from a slurry source 47 is introduced by slurry applicator 46 onto semiconductor device structure 10 and, once slurry 30 has been applied, one or both of semiconductor device structure 10 and polishing pad 40 are substantially continuously laterally moved (e.g., rotate or vibrated or otherwise moved side-to-side) and brought into frictional contact with one another so as so effect the CMP process.

In some instances, it would be desirable to maintain a temperature at or below room temperature during the copper polish (i.e., at or below 74° F. to about 65° F.). This is seldom practical where lower slurry temperature will also result in poor abrasive material dispersal throughout the slurry during polish. Accordingly, elevated temperatures are utilized during the polish. Polishing in all embodiments preferably is conducted at atmospheric pressure and anywhere from 40° F. up to 145° F., although other conditions are of course possible.

Once the desired portions of one or more layers 18, 20 (FIGS. 2-5) have been removed from semiconductor device structure 10, semiconductor device structure 10 is moved away from polishing pad 40 and slurry 30 remaining on semiconductor device structure 10 is rinsed therefrom by a rinse liquid 49 from rinsing element 48. Subsequent fabrication processes may then be conducted on semiconductor device structure 10, as known in the art.

Another polishing format is the so-called “web” format, wherein the pad has an elongate, planar configuration. The web is moved laterally from a supply reel to a take-up reel so as to provide “fresh” areas thereof for polishing one or more layers or structures formed on a semiconductor substrate. A similar, newer, polishing format is the so-called “belt” format, wherein the pad is configured as a belt, or continuous loop, of polishing material. In both the “web” and “belt” formats, the semiconductor substrate is rotated or revolved upon being brought into contact with the pad. The pad is moved when a “fresh” polishing surface is needed or desired.

Example equipment and processing utilized in accordance with the invention is described with reference to FIG. 7, wherein a web-format planarizing machine 60 is used for chemical-mechanical polishing a semiconductor wafer (not shown). Planarizing machine 60 has a support table 62 with a top panel 64 at a work station where an operative portion (A) of a planarizing pad 40′ is positioned. The top-half panel 64 is generally a rigid plate to provide a flat, solid surface to which a particular section of planarizing pad 40′ may be secured during polishing.

Planarizing machine 60 also has a plurality of rollers to guide, position and hold planarizing pad 40′ over top panel 64. The rollers include a supply roller 68, first and second idler rollers 70 a and 70 b, first and second guide rollers 72 a and 72 b, and a take-up roller 74. The supply roller 68 carries an unused or pre-operative portion of the planarizing pad 40′, and take-up roller carries a used or post-operative portion of planarizing pad 40′. First idler roller 70 a and first guide roller 72 a stretch planarizing pad 40′ over top panel 64 to hold the planarizing pad 40′ stationary during operation. Planarizing pad 40′ in accordance with the invention preferably comprises a fixed abrasive pad, such as described above, and having a length greater than a maximum diameter of the wafers being polished. A motor (not shown) derives at least one of supply roller 68 and take-up roller 74 to sequentially advance the planarizing pad 40′ across the top-panel 64. As such, clean pre-operative sections of the planarizing pad 40′ may be quickly substituted for used sections to provide a consistent surface for planarizing and/or cleaning the substrate.

The web-format planarizing machine 60 has a carrier assembly 76 that controls and protects the wafer during polishing. Carrier assembly 76 generally has a substrate holder 78 to pick up, hold and release the wafer at appropriate stages of the polishing cycle. A plurality of nozzles 80 attached to substrate holder 78 dispense a planarizing solution 30′ in accordance with the invention onto a planarizing surface 82 of planarizing pad 40′. Carrier assembly 76 also generally has a support gantry 84 carrying a drive assembly 86 that translates along gantry 84. Drive assembly 86 generally has an actuator 88, a drive shaft 90 coupled to the actuator 88, and an arm 92 projecting from drive shaft 90. Arm 92 carries substrate holder 78 via another shaft 94 such that drive assembly 86 orbits substrate holder 78 about an axis B—B offset from a center point C—C of the wafer.

In accordance with an aspect of the invention, the process preferably comprises moving web/pad 40′ a distance less than the maximum diameter of the wafer such that a subsequently polished wafer is exposed to a fresh pad segment which was not utilized to polish the immediately preceding wafer. Preferably, the distance moved is less than or equal to about 1.0% of the maximum diameter for uniformity of polish and to extend life of the pad. For example for an 8-inch diameter wafer, an incremental movement of pad/web 40′ between each polishing is about 0.25 inch.

In compliance with the statute, the invention has been described in language more or less specific as to structural and methodical features. It is to be understood, however, that the invention is not limited to the specific features shown and described, since the means herein disclosed comprise preferred forms of putting the invention into effect. The invention is, therefore, claimed in any of its forms or modifications within the proper scope of the appended claims appropriately interpreted in accordance with the doctrine of equivalents. The complete disclosures of all patents, patent documents, and publications listed herein are incorporated by reference, as if each were individually incorporated by reference. 

What is claimed is:
 1. A slurry for the chemical-mechanical polishing or planarizing of a copper conductive structure and an adjacent barrier layer of a semiconductor device, the slurry having a pH of about 3 to about 7, and comprising a mixture of an oxidizer, an inhibitor, an abrasive, and water in amounts relative to one another such that when the slurry is in contact with both the copper conductive structure and the adjacent barrier layer, the barrier layer being removed at substantially the same rate or at a slower rate than the copper is removed.
 2. The slurry of claim 1, wherein the relative amounts are balanced so that the barrier layer is oxidized at substantially the same rate as or at a slower rate than the copper is oxidized.
 3. The slurry of claim 1, wherein the relative amounts are balanced so that an oxidation energy of the barrier layer in said slurry is substantially the same as an oxidation energy of copper in the slurry.
 4. The slurry of claim 3, wherein the relative amounts are balanced so that a rate of removal of the barrier layer by the slurry is about up to about ten times slower than a rate of removal of copper by the slurry.
 5. The slurry of claim 3, wherein the relative amounts are balanced so that a rate of removal of the barrier layer by the slurry is about two to about four times less than a rate of removal of copper by the slurry.
 6. The slurry of claim 1, wherein, in the slurry the conductive copper structure and the adjacent barrier layer each having an oxidation energy, the oxidation energy of the barrier layer about 0.25 volt more to about 0.2 volt less than the oxidation energy of the copper conductive structure.
 7. The slurry of claim 1, wherein the barrier layer comprises tungsten.
 8. The slurry of claim 1, in which the oxidizer comprises at least one of an ammonium compound, a nitrate compound, and an amine compound.
 9. The slurry of claim 1, in which the oxidizer is selected from the group consisting of hydrogen peroxide, potassium iodate, potassium permanganate, ammonium persulfate, ammonium molybdate, ferric nitrate, nitric acid, potassium nitrate, ammonia, and other amine compounds, and mixtures thereof.
 10. The slurry of claim 1, comprising about 0.05 to about 10% of the oxidizer, by weight of the slurry.
 11. The slurry of claim 1, in which the inhibitor is selected from the group consisting of benzotriazole, mercaptabenzothiazole, tolytriazole, methylamine, diethylamine, pyridine, quinoline, dicyclohexamine nitrate, potassium silicate, ammonium borate, ammonium phosphate, potassium dichromate, and mixtures thereof.
 12. The slurry of claim 1, comprising about 0.05 to about 2% of the inhibitor, by weight of the slurry.
 13. The slurry of claim 1, in which the abrasive is selected from the group consisting of alumina, titanium dioxide, silicon dioxide, cerium dioxide, and mixtures thereof.
 14. The slurry of claim 1, comprising about 0.05 to about 10% of the abrasive, by weight of the slurry.
 15. The slurry of claim 1, having a pH of between about 3 and about
 5. 16. The slurry of claim 1, further comprising a pH control agent.
 17. The slurry of claim 16, in which the pH control agent is selected from the group consisting of potassium hydrogen phthalate, ammonium acetate, ammonium oxalate, ammonium carbamate, ammonium phosphate, ammonium hydrogen phosphate, ammonium dihydrogen phosphate, dibasic ammonium citrate, tribasic ammonium citrate, acetic acid, phosphoric acid, sulfuric acid, and mixtures thereof.
 18. The slurry of claim 1, further comprising a complexing agent.
 19. The slurry of claim 18, in which the complexing agent is selected from the group consisting of glycine, ammonium citrate, ammonium phosphate, ammonium acetate, ammonium thiocyanate, 2,4-pentadione, and mixtures thereof.
 20. The slurry of claim 1, comprising about 1 to about 10% of the complexing agent, by weight of the slurry.
 21. The slurry of claim 1, further comprising a surfactant.
 22. The slurry of claim 21, in which the surfactant is selected from the group consisting of polyethylene glycol, polyoxyethylene ether, glycerol, polypropylene glycol, polyoxyethylene lauryl ether, polyoxyethylene cetyl ether, polyoxyethylene stearyl ether, polyoxyethylene oleyl ether, and mixtures thereof.
 23. The slurry of claim 1, further comprising a thickener.
 24. A slurry for the chemical-mechanical polishing or planarizing of a copper conductive structure and an adjacent tungsten-containing barrier layer of a semiconductor device, the slurry comprising a mixture of an oxidizer, an inhibitor, an abrasive and water in amounts relative to one another such that when the slurry is in contact with both the copper conductive structure and the adjacent tungsten-containing barrier layer, the tungsten-containing barrier layer being removed at substantially the same rate or at a slower rate than the copper is removed.
 25. The slurry of claim 24, wherein the relative amounts are balanced so that the tungsten-containing barrier layer is oxidized at substantially the same rate as or at a slower rate than the copper is oxidized.
 26. The slurry of claim 24, wherein the relative amounts are balanced so that an oxidation energy of the tungsten-containing barrier layer in said slurry is substantially the same as an oxidation energy of copper in the slurry.
 27. The slurry of claim 26, wherein the relative amounts are balanced so that a rate of removal of the tungsten-containing barrier layer by the slurry is about up to about ten times slower than a rate of removal of copper by the slurry.
 28. The slurry of claim 26, wherein the relative amounts are balanced so that a rate of removal of the tungsten-containing barrier layer by the slurry is about two to about four times less than a rate of removal of copper by the slurry.
 29. The slurry of claim 24, wherein in the slurry the conductive copper structure and the adjacent tungsten-containing barrier layer each having an oxidation energy, the oxidation energy of the tungsten-containing barrier layer about 0.25 volt more to about 0.2 volt less than the oxidation energy of the copper conductive structure.
 30. The slurry of claim 24, wherein the tungsten-containing barrier layer consists essentially of tungsten.
 31. The slurry of claim 24, wherein the tungsten-containing barrier layer comprises greater than about 50% tungsten.
 32. The slurry of claim 24, wherein the tungsten-containing barrier layer comprises a tungsten nitride.
 33. The slurry of claim 24, in which the at least one oxidizer comprises at least one of an ammonium compound, a nitrate compound, and an amine compound.
 34. The slurry of claim 24, in which the oxidizer is selected from the group consisting of hydrogen peroxide, potassium iodate, potassium permanganate, ammonium persulfate, ammonium molybdate, ferric nitrate, nitric acid, potassium nitrate, ammonia, and other amine compounds, and mixtures thereof.
 35. The slurry of claim 24, comprising about 0.05 to about 10% of the oxidizer, by weight of the slurry.
 36. The slurry of claim 24, in which the inhibitor is selected from the group consisting of benzotriazole, mercaptabenzothiazole, tolytriazole, methylamine, diethylamine, pyridine, quinoline, dicyclohexamine nitrate, potassium silicate, ammonium borate, ammonium phosphate, potassium dichromate, and mixtures thereof.
 37. The slurry of claim 24, comprising about 0.05 to about 2% of the inhibitor, by weight of the slurry.
 38. The slurry of claim 24, in which the abrasive is selected from the group consisting of alumina, titanium dioxide, silicon dioxide, cerium dioxide, and mixtures thereof.
 39. The slurry of claim 24, comprising about 0.05 to about 10% of the abrasive, by weight of the slurry.
 40. The slurry of claim 24, having a pH of between about 3 and about
 7. 41. The slurry of claim 24, having a pH of between about 3 and about
 5. 42. The slurry of claim 24, further comprising a pH control agent.
 43. The slurry of claim 42, in which the pH control agent is selected from the group consisting of potassium hydrogen phthalate, ammonium phosphate, ammonium acetate, ammonium dihydrogen phosphate, dibasic ammonium citrate, ammonium hydrogen phosphate, tribasic ammonium citrate, ammonium oxalate, ammonium carbamate, acetic acid, phosphoric acid, sulfuric acid, and mixtures thereof.
 44. The slurry of claim 24, further comprising a complexing agent.
 45. The slurry of claim 44, in which the complexing agent is selected from the group consisting of glycine, ammonium citrate, ammonium phosphate, ammonium acetate, ammonium thiocyanate, 2,4-pentadione, and mixtures thereof.
 46. The slurry of claim 44, comprising about 1 to about 10% of the complexing agent, by weight of the slurry.
 47. The slurry of claim 24, further comprising a surfactant.
 48. The slurry of claim 47, in which the surfactant is selected from the group consisting of polyethylene glycol, polyoxyethylene ether, glycerol, polypropylene glycol, polyoxyethylene lauryl ether, polyoxyethylene cetyl ether, polyoxyethylene stearyl ether, polyoxyethylene oleyl ether, and mixtures thereof.
 49. The slurry of claim 24, further comprising a thickener.
 50. A slurry for the chemical-mechanical polishing or planarizing of a copper conductive structure and an adjacent barrier layer of a semiconductor device, the slurry comprising a mixture of a dual oxidizer, an inhibitor, and an abrasive in amounts relative to one another such that when the slurry is in contact with both the copper conductive structure and the adjacent barrier layer, the adjacent barrier layer being removed at substantially the same rate or at a slower rate than the copper is removed.
 51. The slurry claim 50, wherein the relative amounts are balanced so that the barrier layer is oxidized at substantially the same rate as or at a slower rate than the copper is oxidize.
 52. The slurry of claim 50, wherein the relative amounts are balanced so that an oxidation energy of the barrier layer in said slurry is substantially the same as an oxidation energy of copper in the slurry.
 53. The slurry of claim 52, wherein the relative amounts are balanced so that a rate of removal of the barrier layer by the slurry is about up to about ten times slower than a rate of removal of copper by the slurry.
 54. The slurry of claim 52, wherein the relative amounts are balanced so that a rate of removal of the barrier layer by the slurry is about two to about four times less than a rate of oval of copper by the slurry.
 55. The slurry of claim 50, wherein, in the slurry the conductive copper structure and the adjacent barrier layer each having an oxidation energy, the oxidation energy of the barrier layer about 0.25 volt more to about 0.2 volt less than the oxidation energy of the copper conductive structure.
 56. The slurry of claim 50, wherein the barrier layer consists essentially of tungsten.
 57. The slurry of claim 56, wherein the barrier layer comprises greater than about 50% tungsten.
 58. The slurry of claim 50, wherein the barrier layer comprises a tungsten nitride.
 59. The slurry of claim 50, wherein the dual oxidizer comprises a first oxidizer selected from the group consisting of potassium iodate, potassium permanganate, ferric nitrate, and cerium (IV) compounds such as ceric nitrate and ceric ammonium nitrate, bromates, chlorates, chromates, and iodic acid, ammonia, and other amine compounds, and mixtures thereof; and a minimal amount of a second oxidizer selected from the group consisting of hydrogen peroxide, ammonium persulfate, and mixtures thereof.
 60. The slurry of claim 50, comprising about 0.05 to about 10% of the first oxidizer, by weight of the slurry.
 61. The slurry of claim 50, comprising about 0.001% to about 2% of the second oxidizer, by weight of the slurry.
 62. The slurry of claim 50, in which the inhibitor is selected from the group consisting of benzotriazole, mercaptabenzothiazole, tolytriazole, methylamine, diethylamine, pyridine, quinoline, dicylohexamine nitrate, potassium silicate, ammonium borate, ammonium phosphate, potassium dichromate, and mixtures thereof.
 63. The slurry of claim 50, comprising about 0.05 to about 2% of the inhibitor, by weight of the slurry.
 64. The slurry of claim 50, in which the abrasive is selected from the group consisting of alumina, titanium dioxide, silicon dioxide, cerium dioxide, and mixtures thereof.
 65. The slurry of claim 50, comprising about 0.05 to about 10% of the abrasive, by weight of the slurry.
 66. The slurry of claim 50, having a pH of between about 3 and about
 7. 67. The slurry of claim 50, further comprising a pH control agent selected from the group consisting of potassium hydrogen phthalate, ammonium acetate, ammonium oxalate, ammonium carbamate, ammonium phosphate, ammonium hydrogen phosphate, ammonium dihydrogen phosphate, dibasic ammonium citrate, tribasic ammonium citrate, acetic acid, phosphoric acid, sulfuric acid, and mixtures thereof.
 68. The slurry of claim 50, further comprising a complexing agent selected from the group consisting of glycine, ammonium citrate, ammonium phosphate, ammonium acetate, ammonium thiocyanate, 2,4-pentadione, and mixtures thereof.
 69. The slurry of claim 68, comprising about 1 to about 10% of a complexing agent, by weight of the slurry.
 70. The slurry of claim 50, further comprising a surfactant selected from the group consisting of polyethylene glycol, polyoxyethylene ether, glycerol, polypropylene glycol, polyoxyethylene lauryl ether, polyoxyethylene cetyl ether, polyoxyethylene stearyl ether, polyoxyethylene oleyl ether, and mixtures thereof.
 71. A method for chemical-mechanical polishing a copper structure and an adjacent barrier layer of a semiconductor device structure, comprising: providing a semiconductor device structure including a recess formed in a surface of the device structure, a barrier layer lining at least the recess, and a conductive layer comprising copper over the barrier layer; substantially concurrently polishing the conductive layer and the barrier layer with a slurry having a pH of about 3 to about 7 and comprising a mixture of an oxidizer, an inhibitor, an abrasive, and water in amounts relative to one another such that when the slurry is in contact with both the copper conductive structure and the adjacent barrier layer, the polishing being effected without oxidizing a material of the barrier layer at a substantially greater rate than the copper is oxidized.
 72. The method of claim 71, wherein the step of substantially concurrently polishing comprises employing a slurry formulated to effect an oxidation rate of the barrier layer substantially the same as or less than an oxidation rate of the copper.
 73. The method of claim 71, wherein the step of substantially concurrently polishing comprises employing a slurry formulated to provide a substantially similar oxidation energy of the barrier layer and oxidation energy of the copper.
 74. The method of claim 73, wherein the step of substantially concurrently polishing comprises employing a slurry in which an oxidation energy of the barrier layer is about 0.25 V greater than to about 0.2 V less than an oxidation energy of the copper.
 75. The method of claim 71, wherein the step of substantially concurrently polishing comprises employing a slurry in which a removal rate of a material of the barrier layer is up to about ten times slower than a removal rate of the copper.
 76. The method of claim 71, wherein the step of substantially concurrently polishing comprises employing a slurry in which a removal rate of a material of the barrier layer is about two to about four times slower than a removal rate of the copper.
 77. The method of claim 71, wherein the step of substantially concurrently polishing comprises substantially preventing dissolution of the barrier layer.
 78. The method of claim 71, wherein the step of substantially concurrently polishing is effected at ambient temperature or cooler.
 79. The method of claim 71, wherein the step of providing the semiconductor device structure comprises providing a semiconductor device structure with the barrier layer comprising tungsten.
 80. The method of claim 71, in which the oxidizer of the slurry is selected from the group consisting of hydrogen peroxide, potassium iodate, potassium permanganate, ammonium persulfate, ammonium molybdate, ferric nitrate, nitric acid, potassium nitrate, ammonia, and other amine compounds, and mixtures thereof.
 81. The method of claim 71, in which the slurry comprises about 0.05 to about 10% of the oxidizer, by weight of the slurry.
 82. The method of claim 71, in which the oxidizer of the slurry comprises a dual oxidizer, the dual oxidizer comprising: a first oxidizer selected from the group consisting of potassium iodate, potassium permanganate, ferric nitrate, and cerium (IV) compounds such as ceric nitrate and ceric ammonium nitrate, bromates, chlorates, chromates, and iodic acid, ammonia, and other amine compounds, and mixtures thereof; and a minimal amount of a second oxidizer selected from the group consisting of hydrogen peroxide, ammonium persulfate, and mixtures thereof.
 83. The method of claim 82, comprising about 0.05 to about 10% of the first oxidizer, by weight of the slurry.
 84. The method of claim 82, comprising about 0.001% to about 2% of the second oxidizer, by weight of the slurry.
 85. The method of claim 71, in which the inhibitor of the slurry is selected from the group consisting of benzotriazole, mercaptabenzothiazole, tolytriazole, methylamine, diethylamine, pyridine, quinoline, dicylohexamine nitrate, potassium silicate, ammonium borate, ammonium phosphate, potassium dichromate, and mixtures thereof.
 86. The method of claim 71, in which the slurry comprises about 0.05 to about 2% of the inhibitor, by weight of the slurry.
 87. The method of claim 71, in which the abrasive of the slurry is selected from the group consisting of alumina, titanium dioxide, silicon dioxide, cerium dioxide, and mixtures thereof.
 88. The method of claim 71, in which the slurry comprises about 0.05 to about 10% of the abrasive, by weight of the slurry.
 89. The method of claim 71, in which the slurry further comprises a pH control agent.
 90. The method of claim 71, wherein the pH control agent is selected from the group consisting of potassium hydrogen phthalate, ammonium acetate, ammonium oxalate, ammonium carbamate, ammonium phosphate, ammonium hydrogen phosphate, ammonium dihydrogen phosphate, dibasic ammonium citrate, tribasic ammonium citrate, acetic acid, phosphoric acid, sulfuric acid, and mixtures thereof.
 91. The method of claim 71, in which the slurry further comprises a complexing agent selected from the group consisting of glycine, ammonium citrate, ammonium phosphate, ammonium acetate, ammonium thiocyanate, 2,4-pentadione, and mixtures thereof.
 92. The method of claim 91, in which the slurry comprises about 1 to about 10% of the complexing agent, by weight of the slurry.
 93. The method of claim 71, wherein the barrier layer consists essentially of tungsten.
 94. The method of claim 71, wherein the barrier layer comprises greater than about 50% tungsten.
 95. The method of claim 71, wherein the barrier layer comprises tungsten nitride.
 96. A system for polishing a conductive structure of a semiconductor device, the conductive structure including a conductive region comprising copper and an adjacent tungsten-containing barrier layer, the system comprising: a slurry comprising a mixture of an oxidizer, an inhibitor, an abrasive, and water; the slurry formulated to substantially concurrently polish the conductive region and the tungsten-containing barrier layer so as to remove a material of the tungsten-containing barrier layer at substantially the same rate as or at a slower rate than copper is removed, when the slurry is in contact with both the copper conductive structure and the adjacent tungsten-containing barrier layer.
 97. The system of claim 96, wherein the slurry is formulated to oxidize the copper of the conductive region of the conductive structure at substantially the same rate as or at a faster rate than a material of the barrier layer of the conductive structure is oxidized.
 98. The system of claim 96, wherein the slurry is formulated to oxidize the copper of the conductive region of the conductive structure at substantially the same rate as or at a faster rate than tungsten of the barrier of the conductive structure is oxidized.
 99. The system of claim 96, wherein, in the slurry, a material of the barrier layer of the conductive structure and copper have substantially the same oxidation energies.
 100. The system of claim 96, wherein, in the slurry, the material of the barrier layer of the conductive structure has an oxidation energy of about 0.25 V more to about 0.20 less than an oxidation energy of copper in the slurry.
 101. The system of claim 96, wherein, in the slurry, tungsten of the barrier layer of the conductive structure has an oxidation energy of about 0.25 V more to about 0.20 V less than an oxidation energy of copper in said slurry.
 102. The system of claim 96, wherein, in the slurry, a rate of removal of a material of the barrier layer is up to about ten times slower than a rate of removal of copper.
 103. The system of claim 96, wherein, in the slurry, a rate of removal of a material of the barrier layer is about two to about four times slower than a rate of removal of copper.
 104. The system of claim 96, wherein the slurry is formulated to remove the copper of the conductive region of the conductive structure and tungsten of the barrier layer of the conductive structure without substantially dissolving tungsten of portions of the barrier layer that underlie remaining portions of the conductive region.
 105. The system of claim 96, wherein the slurry is formulated to remove the copper of the conductive region of the conductive structure and a material of the barrier layer of the conductive without substantially dissolving said material in portions of the barrier layer that underlie remaining portions of the conductive region.
 106. The system of claim 96, in which the oxidizer of the slurry comprises at least one of an ammonium compound, a nitrate compound, and an amine compound.
 107. The system of claim 96, in which the oxidizer of the slurry is selected from the group consisting of hydrogen peroxide, potassium iodate, potassium permanganate, ammonium persulfate, ammonium molybdate, ferric nitrate, nitric acid, potassium nitrate, ammonia, and other amine compounds, and mixtures thereof.
 108. The system of claim 96, in which the slurry comprises about 0.05 to about 10% of the oxidizer, by weight of the slurry.
 109. The system of claim 96, in which the oxidizer of the slurry comprises a dual oxidizer, the dual oxidizer comprising: a first oxidizer selected from the group consisting of potassium iodate, potassium permanganate, ferric nitrate, and cerium (IV) compounds such as ceric nitrate and ceric ammonium nitrate, bromates, chlorates, chromates, and iodic acid, ammonia, and other amine compounds, and mixtures thereof; and a minimal amount of a second oxidizer selected from the group consisting of hydrogen peroxide, ammonium persulfate, and mixtures thereof.
 110. The system of claim 109, comprising about 0.05 to about 10% of the first oxidizer, by weight of the slurry.
 111. The system of claim 109, comprising about 0.001% to about 2% of the second oxidizer, by weight of the slurry.
 112. The system of claim 96, in which the inhibitor of the slurry is selected from the group consisting of benzotriazole, mercaptabenzothiazole, tolytriazole, methylamine, diethylamine, pyridine, quinoline, dicylohexamine nitrate, potassium silicate, ammonium borate, ammonium phosphate, potassium dichromate, and mixtures thereof.
 113. The system of claim 96, in which the slurry comprises about 0.05 to about 2% of the inhibitor, by weight of the slurry.
 114. The system of claim 96, in which the abrasive of the slurry is selected from the group consisting of alumina, titanium dioxide, silicon dioxide, cerium dioxide, and mixtures thereof.
 115. The system of claim 96, in which the slurry comprises about 0.05 to about 10% of the abrasive, by weight of the slurry.
 116. The system of claim 96, in which the slurry has a pH of between about 3 and about
 7. 117. The system of claim 96, in which the slurry further comprises a pH control agent.
 118. The system of claim 117, in which the pH control agent is selected from the group consisting of potassium hydrogen phthalate, ammonium acetate, ammonium oxalate, ammonium carbamate, ammonium phosphate, ammonium hydrogen phosphate, ammonium dihydrogen phosphate, dibasic ammonium citrate, tribasic ammonium citrate, acetic acid, phosphoric acid, sulfuric acid, and mixtures thereof.
 119. The system of claim 96, in which the slurry further comprises a complexing agent.
 120. The system of claim 118, in which the complexing agent of the slurry is selected from the group consisting of glycine, ammonium citrate, ammonium phosphate, ammonium acetate, ammonium thiocyanate, 2,4-pentadione, and mixtures thereof.
 121. The system of claim 119, in which the slurry comprises about 1 to about 10% of the complexing agent, by weight of the slurry.
 122. The system of claim 96, in which the slurry further comprises a surfactant.
 123. The system of claim 122, in which the surfactant of the slurry is selected from the group consisting of polyethylene glycol, polyoxyethylene ether, glycerol, polypropylene glycol, polyoxyethylene lauryl ether, polyoxyethylene cetyl ether, polyoxyethylene stearyl ether, polyoxyethylene oleyl ether, and mixtures thereof.
 124. The system of claim 96, wherein the slurry removes copper at a temperature of about 27° C. or less.
 125. A method for formulating a slurry for polishing a conductive structure of a semiconductor device, comprising the step of: selecting and determining concentrations of at least one oxidizer, at least one inhibitor, and at least one abrasive, in which the slurry will oxidize copper at substantially the same rate as or at a faster rate than a tungsten-containing barrier layer material is oxidized.
 126. The method of claim 125, wherein the step of selecting and determining the concentrations comprises evaluating oxidation energies of copper and the barrier layer material in the slurry.
 127. The method of claim 126, wherein the step of selecting and determining the concentrations comprises determining at least one set of concentrations at which the oxidation energies of copper and the barrier layer material are substantially the same.
 128. The method of claim 127, wherein the step of selecting and determining the concentrations comprises determining concentrations at which an oxidation energy of the barrier layer material is about 0.25 V more to about 0.20 V less than an oxidation energy of copper.
 129. The method of claim 125, wherein the step of selecting and determining the concentrations comprises determining concentrations at which a rate of removal of the barrier layer material is up to about ten times slower than a rate of removal of copper.
 130. The method of claim 125, wherein the step of selecting and determining the concentrations comprises determining concentrations at which a rate of removal of the barrier layer material is about two to about four times slower than a rate of removal of copper.
 131. The method of claim 125, wherein the step of selecting and determining the concentrations comprises determining a concentration of the oxidizer within a range of about 0.05 to about 10%, by weight of the slurry.
 132. The method of claim 125, in which the oxidizer of the slurry comprises a dual oxidizer, and the step of selecting and determining the concentrations comprises: determining a concentration of the first oxidizer within a range of about 0.05 to about 10%, by weight of the slurry, and a concentration of the second oxidizer within a range of about 0.001% to about 1%, by weight of the slurry.
 133. The method of claim 125, in which the oxidizer of the slurry comprises a dual oxidizer, and the step of selecting and determining the concentrations comprises: selecting a first oxidizer selected from the group consisting of potassium iodate, potassium permanganate, ferric nitrate, and cerium (IV) compounds such as ceric nitrate and ceric ammonium nitrate, bromates, chlorates, chromates, and iodic acid, ammonia, and other amine compounds, and mixtures thereof; and selecting a minimal amount of a second oxidizer selected from the group consisting of hydrogen peroxide, ammonium persulfate, and mixtures thereof.
 134. The method of claim 125, wherein the step of selecting and determining the concentrations comprises determining a concentration of the inhibitor within a range of about 0.05 to about 2%, by weight of the slurry.
 135. The method of claim 125, wherein the step of selecting and determining the concentrations comprises determining a concentration of the abrasive within a range of about 0.05 to about 10% of the, by weight of the slurry.
 136. A method for chemical-mechanical polishing a copper structure and an adjacent tungsten-containing barrier layer of a semiconductor device structure, comprising: providing a semiconductor device structure including a recess formed in a surface of the device structure, a tungsten-containing barrier layer lining at least the recess, and a conductive layer comprising copper over the tungsten-containing barrier layer; substantially concurrently polishing the conductive layer and the tungsten-containing barrier layer with a slurry comprising a mixture of an oxidizer, an inhibitor, an abrasive, and water in amounts relative to one another such that when the slurry is in contact with both the copper conductive structure and the adjacent tungsten-containing barrier layer, the polishing being effected without oxidizing a material of the tungsten-containing barrier layer at a substantially greater rate than the copper is oxidized.
 137. The method of claim 136, wherein the tungsten-containing barrier layer consists essentially of tungsten.
 138. The method of claim 136, wherein the tungsten-containing barrier layer comprises greater than about 50% tungsten.
 139. The method of claim 136, wherein the tungsten-containing barrier layer comprises a tungsten nitride.
 140. The method of claim 136, in which the slurry has a pH of between about 3 and about
 7. 141. A method for chemical-mechanical polishing a copper structure and an adjacent barrier layer of a semiconductor device structure, comprising: providing a semiconductor device structure including a recess formed in a surface of the device structure, a barrier layer lining at least the recess, and a conductive layer comprising copper over the barrier layer; substantially concurrently polishing the conductive layer and the barrier layer with a slurry comprising a mixture of a dual oxidizer, an inhibitor, an abrasive, and water in amounts relative to one another such that when the slurry is in contact with both the copper conductive structure and the adjacent barrier layer, the polishing being effected without oxidizing a material of the barrier layer at a substantially greater rate than the copper is oxidized.
 142. The method of claim 141, wherein the dual oxidizer comprises: a first oxidizer selected from the group consisting of potassium iodate, potassium permanganate, ferric nitrate, and cerium (IV) compounds such as ceric nitrate and ceric ammonium nitrate, bromates, chlorates, chromates, and iodic acid, ammonia, and other amine compounds, and mixtures thereof; and a minimal amount of a second oxidizer selected from the group consisting of hydrogen peroxide, ammonium persulfate, and mixtures thereof.
 143. The method of claim 142, comprising about 0.05 to about 10% of the first oxidizer, by weight of the slurry.
 144. The method of claim 142, comprising about 0.001% to about 2% of the second oxidizer, by weight of the slurry.
 145. A system for polishing a conductive structure of a semiconductor device, the conductive structure including a conductive region comprising copper and an adjacent barrier layer, the system comprising: a slurry having a pH of about 3 to about 7 and comprising a mixture of an oxidizer, an inhibitor, an abrasive, and water; the slurry formulated to substantially concurrently polish the conductive region and the barrier layer so as to remove a material of the barrier layer at substantially the same rate as or at a slower rate than copper is removed, when the slurry is in contact with both the copper conductive structure and the adjacent barrier layer.
 146. A system for polishing a conductive structure of a semiconductor device, the conductive structure including a conductive region comprising copper and an adjacent barrier layer, the system comprising: a slurry comprising a mixture of a dual oxidizer, an inhibitor, an abrasive, and water; the slurry formulated to substantially concurrently polish the conductive region and the barrier layer so as to remove a material of the barrier layer at substantially the same rate as or at a slower rate than copper is removed, when the slurry is in contact with both the copper conductive structure and the adjacent barrier layer.
 147. The slurry of claim 146, wherein the dual oxidizer comprises: a first oxidizer selected from the group consisting of potassium iodate, potassium permanganate, ferric nitrate, and cerium (IV) compounds such as ceric nitrate and ceric ammonium nitrate, bromates, chlorates, chromates, and iodic acid, ammonia, and other amine compounds, and mixtures thereof; and a minimal amount of a second oxidizer selected from the group consisting of hydrogen peroxide, ammonium persulfate, and mixtures thereof.
 148. A method for formulating a slurry for polishing a conductive structure of a semiconductor device, comprising the step of: selecting and determining concentrations of at least one oxidizer, at least one inhibitor, and at least one abrasive, in which the slurry has a pH of about 3 to about 7, and will oxidize copper at substantially the same rate as or at a faster rate than a barrier layer material is oxidized.
 149. A method for formulating a slurry for polishing a conductive structure of a semiconductor device, comprising the step of: selecting and determining concentrations of a dual oxidizer, at least one inhibitor, and at least one abrasive, in which the slurry will oxidize copper at substantially the same rate as or at a faster rate than a barrier layer material is oxidized.
 150. The method of claim 149, wherein the step of selecting and determining the concentration of the dual oxidizer comprises: selecting a first oxidizer selected from the group consisting of potassium iodate, potassium permanganate, ferric nitrate, and cerium (IV) compounds such as ceric nitrate and ceric ammonium nitrate, bromates, chlorates, chromates, and iodic acid, ammonia, and other amine compounds, and mixtures thereof; and selecting a minimal amount of a second oxidizer selected from the group consisting of hydrogen peroxide, ammonium persulfate, and mixtures thereof.
 151. The method of claim 149, wherein the step of selecting and determining the concentration of the dual oxidizer comprises: determining a concentration of the first oxidizer within a range of about 0.05 to about 10%, by weight of the slurry, and a concentration of the second oxidizer within a range of about 0.001% to about 1%, by weight of the slurry. 